Methods and Compositions for Digestion of Organic Waste

ABSTRACT

The present invention relates to a process wherein organic material derived from plant and animal material is processed to recover nutritional elements. In particular, there is provided a process for releasing nutritional elements from plant and animal material comprising the steps of treating the material with one or more enzymes to digest said material under appropriate conditions and separating the resulting liquid hydrolysate from the undigested material.

RELATED APPLICATIONS

This application claims the benefit of U.S. Provisional Application Ser.No. 61/015,531, filed on Dec. 20, 2007; the entire contents of theapplication is incorporated herein by reference.

BACKGROUND OF THE INVENTION

The processing and disposal of organic waste streams are increasinglyimportant topics of environmental, economical and technological concern.Organic waste is generated from different activities, such as industrialactivities (e.g., organic waste from food processing manufacturers,restaurants, and grocery stores), agricultural activities (e.g., organicwaste from gardens, farms, or cattle farms), and domestic activities(e.g., household waste). There are increasing problems in the handlingof these plant and animal organic waste streams due to the continuouslyincreasing amount produced. The problems are global in nature, but areparticular acute in areas with very dense human populations and in areaswith intense livestock production.

Traditional solutions to the problem of disposing of organic waste, suchas landfill, incineration, or composting, are associated with variousproblems, e.g., processing space, building and operating costs,consumption of time resources, and environmental pollution. Thus, thereis an environmental and industrial need to find methods and processesthat, as opposed to disposal, allow for the recovery, release and/orutilization of the valuable nutrients in organic waste.

In this respect, several solutions have been proposed in the art.However, none is suitable for the processing of fresh organic waste,e.g., fresh food waste, as presented, for example, in supermarketorganic waste, into nutrients that are in a bioavailable form. Forexample, discussed in US Publication 26194299 (Brinch-Pedersen et al.)is a method for recycling slurry or sewage waste material (e.g., manure)derived from human, animal and industrial areas which must first beseparated into liquid and solid fractions. U.S. Pat. No. 6,121,032(Cooney Jr. et al.) teaches processes and compositions which may be usedfor facilitating the decomposition of foodstuff waste solids which areto be provided to a sewage treatment system (e.g., garbage disposal andseptic tanks).

In contrast to the above-identified solutions proposed in the art, it isone signifimayt object of the present invention to provide a process forreleasing and recycling important nutritional elements derived fromorganic waste in a bioavailable form. The inventors of the presentinvention have found that there is a large potential for using variouskinds of enzymes for solubilizing important nutritional elements presentin organic waste (e.g., fresh food waste), thereby facilitating therelease and increased availability of the important nutritional elementsin a bioavailable form.

The process of the invention has the advantages of being capable of 1)giving a very high degree of released valuable nutritional elements fromorganic waste, including undenatured protein, natural oils, activeenzymes, plant hormones, aerobic bacteria, and aerobic fungi, 2)reducing the overall cost and time for the treatment of waste, 3)increasing environmental sustainability and 4) sequestering of thecarbon molecules.

In particular, the sequestering of the carbon molecules is accomplishedby keeping the carbon within the end product in accordance with thefollowing principles:

1. The use of fresh organic waste with minimized decomposition preventsthe formation of gas (e.g., carbon dioxide (CO₂) and/or methane (CH₄)).Therefore, at the start of the enzymatic digestion processes asdescribed herein, all of the original carbon content of the organicwaste (e.g., fresh food waste) is present;

2. The process is done rapidly and aerobically. in order to minimizedecomposition;

3. The resulting hydrolysate may be stabilized (e.g., using acidstabilization) such that decomposition of the enzymatically digestedorganic material has been minimized and stabilized and is thereforestill ‘fresh’ when it is applied to the soil;

4. The resulting hydrolysate may be applied to soil as a fertilizer andthis ‘fresh’ product—hydrolyzed food in its natural state—may becomefood for aerobic soil microbes living in the root zone of the plant.Soil microbes may turn the carbon in this material into plant availablenutrients. The carbon is taken up directly into the plant and convertedinto plant material such that the carbon originally present in theinitial organic waste is sequestered and incorporated back into plants;and

5. By supplanting the use of petro-chemical fertilizers and/or compost,carbon sequestration accomplished as described herein helps to preventthe leaching of carbon into the water supply or into the atmosphere bythe 50-80% of all chemical fertilizers, including reduction of ammoniavolatilization, which turns urea into ammonia gas, and denitrification,where nitrate-N is converted into gaseous forms (nitric oxide, nitrousoxide, dinitrogen). Similarly, supplanting of composting producessimilar benefits as a typical compost pile will reduce its size by 50%,of which some signifimayt portion is due to the leaching of carbon intothe groundwater and more still is gassed off as carbon dioxide andmethane.

SUMMARY OF THE INVENTION

The present invention is based, in part, on the discovery that theprocesses described herein provide for releasing and recycling importantnutritional elements derived from organic waste in a bioavailable form.

Accordingly, in one aspect, the invention features a process for therelease of nutritional elements from organic waste comprising the stepsof: (a) adding to said organic waste at least one enzyme or at least onemixture of enzymes; (b) incubating the organic waste of step (a) underappropriate conditions resulting in at least partial release of thenutritional elements as a liquid hydrolysate; and (c) separation of theundigested waste from the resulting liquid hydrolysate. In oneembodiment, the organic waste is fresh food waste.

The enzymes used in step (a) may comprise at least two or more, e.g.,three, four, five, six, seven, eight, nine, or ten enzymes. The two ormore enzymes may be added together or sequentially to the organic wastein step (a). In another aspect, the two or more enzymes may be selectedfrom the group consisting of xylanase, asparaginase, cellulase,hemicellulase, glumayase, beta-glumayase (endo-1,3(4)-), urease,protease, lipase, amylase, phytase, phosphatase, aminopeptidase,amylase, carbohydrase, carboxypeptidase, catalase, chitinase, cutinase,cyclodextrin glycosyltransferase, deoxyribonuclease, esterase,alpha-galactosidase, beta-galactosidase, glucoamylase, alpha-amylase,alpha-glucosidase, beta-glucosidase, haloperoxidase, invertase, laccase,mannosidase, oxidase, glucose oxidase, pectinolytic enzyme,pectinesterase, peptidoglutaminase, peroxidase, polyphenoloxidase,proteolytic enzyme, protease, ribonuclease and transglutaminase. Theseenzymes may be selected, for example, from the group consisting ofenzymes originating from microbial fermentation, enzymes derived from amicroorganism, and enzymes derived from plants.

The incubating organic waste of step (b) may be under constant movement.In another aspect, the temperature of the incubating organic waste ofstep (b) is between 70° F. and 162° F. (e.g., between 125° F. and 140°F.). In yet another aspect, the incubating organic waste of step (b) maybe incubated for between 0 hours and 2.5 hours (e.g., between 45 minutesand 1.5 hours). In one embodiment, the incubating organic waste of step(b) may output a liquid hydrolysate that is greater than 70 percent(e.g., greater than 90 percent) by weight relative to the weight of theinput incubating organic waste.

The process separation step of step (c) may exclude undigested materialof greater than 0.5 millimeters (e.g., greater than 1 mm) in diameterfrom the liquid hydrolysate.

In another aspect, the invention features a process for the release ofnutritional elements from organic waste comprising the steps of: (a)adding to said organic waste at least one enzyme or at least one mixtureof enzymes; (b) incubating the organic waste of step (a) underappropriate conditions resulting in at least partial release of thenutritional elements as a liquid hydrolysate; (c) separation of theundigested waste from the resulting liquid hydrolysate. In oneembodiment, the organic waste is fresh food waste; and (d) stabilizationof the liquid hydrolysate resulting from step (c).

The enzymes used in step (a) may comprise at least two or more, e.g.,three, four, five, six, seven, eight, nine, or ten enzymes. The two ormore enzymes may be added together or sequentially to the organic wastein step (a). In another aspect, the two or more enzymes may be selectedfrom the group consisting of xylanase, asparaginase, cellulase,hemicellulase, glumayase, beta-glumayase (endo-1,3(4)-), urease,protease, lipase, amylase, phytase, phosphatase, aminopeptidase,amylase, carbohydrase, carboxypeptidase, catalase, chitinase, cutinase,cyclodextrin glycosyltransferase, deoxyribonuclease, esterase,alpha-galactosidase, beta-galactosidase, glucoamylase, alpha-amylase,alpha-glucosidase, beta-glucosidase, haloperoxidase, invertase, laccase,mannosidase, oxidase, glucose oxidase, pectinolytic enzyme,pectinesterase, peptidoglutaminase, peroxidase, polyphenoloxidase,proteolytic enzyme, protease, ribonuclease and transglutaminase. Theseenzymes may be selected, for example, from the group consisting ofenzymes originating from microbial fermentation, enzymes derived from amicroorganism, and enzymes derived from plants.

The incubating organic waste of step (b) may be under constant movement.In another aspect, the temperature of the incubating organic waste ofstep (b) is between 70° F. and 162° F. (e.g., between 125° F. and 140°F.). In yet another aspect, the incubating organic waste of step (b) maybe incubated for between 0 hours and 2.5 hours (e.g., between 45 minutesand 1.5 hours). In one embodiment, the incubating organic waste of step(b) may output a liquid hydrolysate that is greater than 70 percent(e.g., greater than 90 percent) by weight relative to the weight of theinput incubating organic waste.

The process separation step of step (c) may exclude undigested materialof greater than 0.5 millimeters (e.g., greater than 1 mm) in diameterfrom the liquid hydrolysate.

The process stabilization step of step (d) may comprise addition andmixing of the liquid hydrolysate with an acid source. In one embodiment,the acid source may be selected from the group consisting ofhydrochloric, sulfuric, phosphoric, acetic, stearic, propionic,tartaric, maleic, benzoic, or succinic acids. In another embodiment, thepH of the liquid hydrolysate is less than 7.0 (e.g., the pH of theliquid hydrolysate is 3.5).

In yet another aspect, the invention features a process for the releaseof nutritional elements from organic waste comprising the steps of: (a)adding to said organic waste at least one enzyme or at least one mixtureof enzymes; (b) incubating the organic waste of step (a) underappropriate conditions resulting in at least partial release of thenutritional elements as a liquid hydrolysate; (c) coarse separation ofthe undigested waste from the resulting liquid hydrolysate. In oneembodiment, the organic waste is fresh food waste; (d) stabilization ofthe liquid hydrolysate resulting from step (c); and (e) fine separationof the undigested waste from the resulting liquid hydrolysate.

The enzymes used in step (a) may comprise at least two or more, e.g.,three, four, five, six, seven, eight, nine, or ten enzymes. The two ormore enzymes may be added together or sequentially to the organic wastein step (a). In another aspect, the two or more enzymes may be selectedfrom the group consisting of xylanase, asparaginase, cellulase,hemicellulase, glumayase, beta-glumayase (endo-1,3(4)-), urease,protease, lipase, amylase, phytase, phosphatase, aminopeptidase,amylase, carbohydrase, carboxypeptidase, catalase, chitinase, cutinase,cyclodextrin glycosyltransferase, deoxyribonuclease, esterase,alpha-galactosidase, beta-galactosidase, glucoamylase, alpha-amylase,alpha-glucosidase, beta-glucosidase, haloperoxidase, invertase, laccase,mannosidase, oxidase, glucose oxidase, pectinolytic enzyme,pectinesterase, peptidoglutaminase, peroxidase, polyphenoloxidase,proteolytic enzyme, protease, ribonuclease and transglutaminase. Theseenzymes may be selected, for example, from the group consisting ofenzymes originating from microbial fermentation, enzymes derived from amicroorganism, and enzymes derived from plants.

The incubating organic waste of step (b) may be under constant movement.In another aspect, the temperature of the incubating organic waste ofstep (b) is between 70° F. and 162° F. (e.g., between 125° F. and 140°F.). In yet another aspect, the incubating organic waste of step (b) maybe incubated for between 0 hours and 2.5 hours (e.g., between 45 minutesand 1.5 hours). In one embodiment, the incubating organic waste of step(b) may output a liquid hydrolysate that is greater than 70 percent(e.g., greater than 90 percent) by weight relative to the weight of theinput incubating organic waste.

The process separation step of step (c) may exclude undigested materialof greater than 0.5 millimeters (e.g., greater than 1 mm) in diameterfrom the liquid hydrolysate.

The process stabilization step of step (d) may comprise addition andmixing of the liquid hydrolysate with an acid source. In one embodiment,the acid source may be selected from the group consisting ofhydrochloric, sulfuric, phosphoric, acetic, stearic, propionic,tartaric, maleic, benzoic, or succinic acids. In another embodiment, thepH of the liquid hydrolysate is less than 7.0 (e.g., the pH of theliquid hydrolysate is 3.5).

The process separation step of step (e) may exclude undigested materialof greater than 149 microns (e.g., greater than 300 microns) in diameterfrom the liquid hydrolysate.

In still another aspect of the invention, the organic waste to bedigested in any of the processes described herein may first be groundinto particles prior to enzymatic digestion (e.g., first ground intoparticles less than ⅜ inch in diameter). In another embodiment, theliquid hydrolysate resulting from any of the processes described hereinmay be used as a nutraceutical, organic fertilizer, pharmaceutical,aquaculture feed, animal feed, or biostimulant. In still anotherembodiment, the liquid hydrolysate resulting from any of the processesdescribed herein may be used as an enhanced feedstock of bioavailablenutrients for anaerobic or aerobic fermentation useful for theproduction of chemicals (e.g., biogases, biofuels, and alcohols).

In yet another aspect, the present invention provides an enzyme mixturecomprising at least two enzymes, e.g., such as three, four, five, six,seven, eight, nine or ten enzymes, selected from the group consisting ofxylanase, asparaginase, cellulase, hemicellulase, glumayase,beta-glumayase (endo-1,3(4)-), urease, protease, lipase, amylase,phytase, phosphatase, aminopeptidase, amylase, carbohydrase,carboxypeptidase, catalase, chitinase, cutinase, cyclodextringlycosyltransferase, deoxyribonuclease, esterase, alpha-galactosidase,beta-galactosidase, glucoamylase, alpha-amylase, alpha-glucosidase,beta-glucosidase, haloperoxidase, invertase, laccase, mannosidase,oxidase, pectinolytic enzyme, peptidoglutaminase, peroxidase,polyphenoloxidase, proteolytic enzyme, protease, ribonuclease andtransglutaminase, or combinations thereof.

In a still further aspect, the invention relates to the use of theenzyme mixture according to the invention for releasing nutritionalelements from organic waste according to any of the processes describedherein.

DETAILED DESCRIPTION OF THE INVENTION

It is a primary object of the present invention to provide a process forreleasing and recycling important nutritional elements derived fromorganic waste in a bioavailable form.

The inventors of the present invention have found that it is possible toutilize the resources present in organic waste by turning them intoimportant and valuable nutritional elements. The methods andcompositions of the invention allow the release of nutritional elementsfrom organic waste through treatment with enzymes that, for example, andwithout limitation, degrade fats and oils (e.g., lipases), protein(e.g., proteases), starch (e.g., carbohydrases), sugars (e.g., glucoseoxidases), fruit/pectin (e.g., pectinesterases), cellulose (e.g.,cellulases), and/or hemicellulose (e.g., hemicellulases).

In addition, the inventors realized that bioavailability of the releasednutrients derived from the enzymatically digested organic material maybe improved by incorporating the step of stabilizing the liquidhydrolysate that is reacted by the enzymatic digestion of the organicmaterial.

One will realize that the fresh organic material to be digested may bean important element for the methods of the present invention, in orderto recycle important nutritional elements within using an enzymaticdigestion process.

Thus, in an aspect of the present invention, there is provided a processfor releasing nutritional elements from organic waste, the processcomprising the steps of:

(a) adding to said organic waste at least one enzyme or at least onemixture of enzymes;

(b) incubating the organic waste of step (a) under appropriateconditions resulting in at least partial release of the nutritionalelements as a liquid hydrolysate; and

(c) separation of the undigested waste from the resulting liquidhydrolysate.

In another embodiment, the process according to the invention, comprisesthe steps of:

(a) adding to said organic waste at least one enzyme or at least onemixture of enzymes;

(b) incubating the organic waste of step (a) under appropriateconditions resulting in at least partial release of the nutritionalelements as a liquid hydrolysate;

(c) separation of the undigested waste from the resulting liquidhydrolysate; and

(d) stabilization of the liquid hydrolysate resulting from step (c).

In yet a further embodiment, the process according to the invention,comprises the steps of:

(a) adding to said organic waste at least one enzyme or at least onemixture of enzymes;

(b) incubating the organic waste of step (a) under appropriateconditions resulting in at least partial release of the nutritionalelements as a liquid hydrolysate;

(c) coarse separation of the undigested waste from the resulting liquidhydrolysate;

(d) stabilization of the liquid hydrolysate resulting from step (c); and

(e) fine separation of the undigested waste from the resulting liquidhydrolysate.

In some embodiments of the present invention the nutritional elements ornutrients are selected from the group consisting of plant nutrients,metals, minerals, carbohydrates, peptides, and oils. In otherembodiments, the plant nutrients are selected from the group consistingof phosphate, calcium, potassium, and nitrogen. In yet anotherembodiment of the present invention, the plant nutrient is phosphate,such as organic phosphate or inorganic orthophosphate.

In the present context, the terms “waste” and “organic waste” are usedinterchangeably and refer to any type of discarded organic materialderived from human, animal or industrial areas. In one embodiment, thewaste is selected from the group consisting of municipal sewage,household waste, slaughterhouse waste, human waste, plant waste such asfrom gardening, animal waste and industrial waste such as waste from thefood, feed and pharmaceutical industry, e.g. waste from fermentationprocesses, brewing or production of recombinant enzymes. The waste maybe provided from waste holding facilities, i.e., facilities for holding,storage or treatment of waste, including pits or lagoon where animalwaste is stored. In the present context, the terms “fresh food waste”and “fresh food organic waste” are used interchangeably and refer towaste which has the following characteristics: 1. the fresh food wasteis substantially firm with a shiny color, 2. any flesh willsubstantially spring back when pressed, 3. the fresh food waste issubstantially free of discoloration or darkening around the edges, 4.the fresh food waste will smell substantially fresh and be substantiallyfree of any ammonia, “rotten egg,” “fishy,” or other foul smell, 5.juice will not have substantially seeped from a substantial amount offruit, and 6. the fresh food waste has been kept substantially at anappropriate temperature (e.g., constant refrigeration) to maintainfreshness. By contrast, “decomposition” or “decomposing waste” refers toprocesses or material for which at least one of the followingcharacteristics is present: 1. the waste is substantially soft with adull color, 2. any flesh will not substantially spring back when pressedor has lost its shape or firmness, 3. the waste has substantialdarkening around the edges, or substantial brown, black, green or yellowdiscoloration, 4. the waste emits a substantial foul odor, including,but not limited to the scent of ammonia, “rotten egg,” “fishy,” vinegar,yeast, or mold, 5. fungal (mold) or bacterial growth is substantiallypresent, or 6. the waste has not substantially been kept at anappropriate temperature to ensure freshness. With regard to thesecriteria, the terms “substantial” and “substantially” may refer to 50%,55%, 60%, 65%, 70%, 71%, 72%, 73%, 74%, 75%, 76%, 77%, 78%, 79%, 80%,81%, 82%, 83%, 84%, 85%, 86%, 87%, 88%, 89%, 90%, 91%, 92%, 93%, 93%,94%, 95%, 96%, 97%, 98%, 99%, 99.5%, 99.9%, or greater of the organicwaste as a whole or characteristic of particular elements of the organicwaste under consideration.

The use of fresh food waste may be critical for obtaining as high acontent of nutrients as possible from the waste. Through carefulobservation, the present inventors have identified processes thatminimize decomposition of organic waste such that it is kept in a freshstate. In one embodiment, the processes of the invention involves theuse of organic waste, e.g., fresh food waste, specifically subjected tohandling conditions that minimize degradation, decomposition, or aninitial release of nutrients and carbohydrates. In one embodiment, thefresh food waste may be provided from waste holding facilities, e.g.facilities for holding, storage or treatment of fresh food waste,including supermarket facilities. For example, pre-weighed containersmay be filled with fresh food waste such that the weight of the freshfood waste contents is known and tracked (e.g., by a barcode and/orcomputer tracking system). The containers may be cleaned and sterilizedprior to being used to collect fresh food waste according to methodswell known in the art. In another embodiment, the containers may beinsulated in order to help ensure appropriate temperatures required tomaintain freshness, and/or hold relatively small volumes of fresh foodwaste (e.g., 1,000 pounds or less), and/or have sealable lids to helpensure freshness. In still other embodiments, the containers may becollected frequently (e.g., three days per week) and transported to aprocessing facility, optionally, using refrigerated conditions duringtransport (e.g., refrigerated trucks). The organic waste, e.g., freshfood waste, may optionally be source separated into separate categoriesof waste, e.g., vegetable waste versus animal meat waste. In the foodindustry, the term “source separation” typically refers to thesequestration of trash components (e.g., paper, plastic, “rubbish”,cardboard, glass, newspaper, and aluminum and steel mays) away fromorganic waste. In addition to this common definition within the art, theterm “source separation” may alternatively refer to the sequestration ofdifferent types of organic waste streams (e.g., bakery, deli, seafood,produce, and packaged goods) whether they contain trash components ornot. Through careful observation, the present inventors determined thatisolation of different types of organic waste streams allows for theproduction of consistent and defined commingled raw material forenhanced digestion by the enzymes described herein. In this respect, theproportion of trash components present within the raw organic materialto be digested may be 1%, 2%, 3%, 4%, 5%, 10%, 20%, 30%, 40%, 50%, ormore by weight or volume of the raw organic material or any range inbetween to be digested since these components will subsequently beremoved when the resulting liquid hydrolysate is separated from theundigested waste. In addition, the organic waste to be enzymaticallydigested, e.g., fresh food waste, does not need to be separatedaccording to liquid and solid phases.

Optionally, the organic waste, e.g., fresh food waste, is ground intoparticles of a defined average size. The ground particles, on average,may have a length of any side less than 10 inches, 9 inches, 8 inches, 7inches, 6 inches, 5 inches, 4 inches, 3 inches, 2 inches, 1 inch, ⅞inch, ¾ inch, ⅝ inch, ½ inch, ⅜ inch, ¼ inch, ⅛ inch, 1/16 inch or less.

In a further step of the present invention, the organic waste, e.g.,fresh food waste, is subjected to an enzymatic digestion step, which isachieved by treatment with one or more appropriate enzymes. In oneembodiment, two or more enzymes, e.g., three, four, five, six, seven,eight, nine or ten enzymes, are added to the organic waste, e.g., freshfood waste.

In another embodiment, the enzyme(s) is selected from the groupconsisting of xylanase, asparaginase, cellulase, hemicellulase,glumayase, beta-glumayase (endo-1,3(4)-), urease, protease, lipase,amylase, phytase, phosphatase, aminopeptidase, amylase, carbohydrase,carboxypeptidase, catalase, chitinase, cutinase, cyclodextringlycosyltransferase, deoxyribonuclease, esterase, alpha-galactosidase,beta-galactosidase, glucoamylase, alpha-amylase, alpha-glucosidase,beta-glucosidase, haloperoxidase, invertase, laccase, mannosidase,oxidase, glucose oxidase, pectinolytic enzyme, pectinesterase,peptidoglutaminase, peroxidase, polyphenoloxidase, proteolytic enzyme,protease, ribonuclease and transglutaminase, or combinations hereof. Theaddition of xylanase, asparaginase, glumayase, beta-glumayase(endo-1,3(4)-) and cellulase results in a degradation of the cell wallof the lignocellulosic material present in the waste, whereas theprotease degrades protein, lipase degrades lipid and starch is degradedby the addition of amylase and carbohydrase. The skilled artisan willappreciate that particular enzymes with substantially the same functionsas those enzymes listed above are well known in the art, including theparameters required for determining optimal enzymatic activity anddetermining cohabitability with other enzymes such that all enzymes thatcohabitat are functionally active. For example, 0.01 g, 0.05 g, 0.1 g,0.15 g, 0.2 g, 0.25 g, 0.3 g, 0.35 g, 0.4 g, 0.45 g, 0.5 g, 0.55 g, 0.6g, 0.65 g, 0.7 g, 0.75 g, 0.8 g, 0.85 g, 0.9 g, 0.95 g, 1.0 g (i.e., theweight of 50 mL of enzyme given that the density of the enzymessolutions is similar to that of water), 1.05 g, 1.1 g, 1.15 g, 1.20 g,1.25 g, 1.30 g, 1.35 g, 1.40 g, 1.45 g, 1.50 g, 1.55 g, 1.60 g, 1.65 g,1.70 g, 1.75 g, 1.80 g, 1.85 g, 1.90 g, 1.95 g, 2.00 g, or more or anyrange in between of per each enzyme(s) (e.g., Asparaginase (3,500ASNU/g, Acrylaway® L, Novozymes, Inc.), Beta-glucanase (endo-1,3(4)-)(100 FBG/g, Peelzym® or Viscozyme® L, Novozymes, Inc.), Cellulase (700EGU/g, Celluclast®, 1.5L, Lot #CCN03079, Novozymes, Inc.), Protease (2.4AU-A/g, Alcalase 2.4 LFG®, Lot #PLN05317, Novozymes, Inc.),Alpha-amylase (400 KNU-B/g, Ban 480L®, Lot #ADN04234 or LiquozymeSupra®, Lot #NBPG002, Novozymes, Inc.), Lipase (100 KLU/g, Greasex100L®, Lot #LAP40013, Novozymes, lnc.), Pectinase (Pectinex 100L Plus®,Lot #KV5530100, Novozymes, Inc.), Glucoamylase (Dextrozyme DX®, Lot#NCPP0044, Novozymes, Inc.), and/or Xyalanase (Shearzyme 500L®, Lot#CDN00243, Novozymes, Inc.) may be added per 8×10⁴ gram basis of organicwaste.

If the enzymes are added together to the solid waste phase, the enzymesmay be added as a mixture or cocktail of enzymes or as a compositioncomprising multiple enzymatic activities. Such a mixture or compositionmay be a commercial product or be prepared on site. In one embodiment,the mixture of enzymes comprises at least two enzymes, e.g., three,four, five, six, seven, eight, nine or ten enzymes, selected from thegroup consisting of xylanase, asparaginase, cellulase, hemicellulase,glumayase, beta-glumayase (endo-1,3(4)-), urease, protease, lipase,amylase, phytase, phosphatase, aminopeptidase, amylase, carbohydrase,carboxypeptidase, catalase, chitinase, cutinase, cyclodextringlycosyltransferase, deoxyribonuclease, esterase, alpha-galactosidase,beta-galactosidase, glucoamylase, alpha-amylase, alpha-glucosidase,beta-glucosidase, haloperoxidase, invertase, laccase, mannosidase,oxidase, glucose oxidase, pectinolytic enzyme, pectinesterase,peptidoglutaminase, peroxidase, polyphenoloxidase, proteolytic enzyme,protease, ribonuclease and transglutaminase, or combinations thereof.Examples of mixtures or compositions are described herein.

In one embodiment of the present invention, the enzymatic treatment isperformed with an enzyme(s) selected from the group consisting of anenzyme(s) which originates from microbial fermentation, enzyme(s)derived from a microorganism, such as a genetic engineeredmicroorganism, or enzyme(s) derived from a plant, e.g., a geneticallyengineered plant.

In accordance with the present invention, the organic waste, e.g., freshfood waste, to be digested is kept under appropriate conditionsresulting in at least partial release of the nutritional elements duringthe enzymatic digestion process. In the present context, the expression“appropriate conditions” relates to a specific temperature, time, pH,pressure, and mechanical force in accordance with the enzyme or enzymesused. The organic waste may be digested, i.e., bonds are cleaved,without, or with minimized, decomposition.

In one embodiment, the process temperature, i.e., the temperature duringthe enzymatic digestion, may be between 0° F. and 165° F., such asbetween 70° F. and 162° F., or 70° F. and 155° F., or 125° F. and 140°F., or any range in between. In another embodiment, the temperatureduring the enzymatic digestion is 132.5° F. The process temperatureshould be below about 140° F. in order to prevent decomposition of theprotein components within the digested sample. In some embodiments, thetemperature at which the enzymatic digestion step occurs is less thanabout 140° F. However, it will be appreciated that the temperatureemployed may be within the optimum temperature of the enzyme(s) used inthe process. A skilled artisan will also appreciate that lowerincubation temperatures may be compensated with longer incubation timesor a higher relative concentration of the enzymatic composition, orboth.

In one embodiment, the process pH, i.e., the pH during the enzymaticdigestion, may be between 0 and 7.0 including any range in between(e.g., 4.5 to 5.0). A skilled artisan will appreciate that differentenzymes optimally operate within different pH ranges. In one embodiment,enzymes are selected such that they may cohabitate and maintain theirfunction in a neutral or acidic environment. In general, organic wastedigested using the processes described herein have a pH within the rangeof 4.5 to 5.0. In many cases, the enzymatic digestion treatment may becarried out with satisfactory results without any adjustment of the pHbefore, or during, the performance of the treatment. However, for sometypes of waste materials, it may be advantageous to adjust the pH of thewaste material prior to or during enzymatic digestion. The pH may bedecreased, i.e., acidic conditions or the pH of the reaction mixture maybe increased by adding appropriate amounts of an acid or base,respectively, and/or a buffer system according to methods well known inthe art. However, it will be appreciated that the pH employed may bewithin the optimum pH range of the enzyme(s) used in the process.

It has been the inventors' observation that by sustaining a constantmovement of the organic waste, e.g., fresh food waste, the digestion isimproved. Thus, in one embodiment, the enzymatic digestion step, orduring all the steps of the present process, is under constantagitation, shear, and/or pressure. For example, an enzymatic digestionapparatus may contain a rotating shaft driven by a motor to which isfixed two screws oriented in opposite directions such that mechanicalshear forces are exerted against the digesting organic material withinthe fixed enclosure.

The time allotted for the enzymatic digestion in the methods of thepresent invention is such that nutrient recovery from the digestedorganic waste occurs, e.g., fresh food waste, in a bioavailable form.The process time is generally between 0 hours and about 2.5 hours. Thebatch may be brought uniformally up to a desired temperature. From thatpoint, it may take between from about 45 minutes to about 1.5 hours. Thetime is determined by when the material has reached its maximum yield.In one embodiment, the maximum yield occurs at 20%, 30%, 40%, 50%, 60%,70%, 75%, 80%, 81%, 82%, 83%, 84%, 85%, 86%, 87%, 88%, 89%, 90%, 91%,92%, 93%, 94%, 95%, 96%, 97%, 98%, 99%, 99.5% or greater hydrolysis(i.e., % weight of free flowing liquid hydrolysate relative to the totalinput weight of the organic material to be digested) or any range inbetween. In one embodiment, an enhanced yield occurs when the batchis >90% hydrolyzed. In another embodiment, the conditions in which theenzymatic digestion is performed are such that, upon completion of thereaction, a hydrolysate containing peptides with an average molecularweight less than 1, 10, 100, 200, 300, 400, 500, 600, 700, 800, 900,1000 Daltons, such as less than 1, 1.5, 2, 2.5, 3, 3.5, 4, 4.5, 5, 5.5,6, 6.5, 7, 7.5, 8, 8.5, 9, 9.5, or 10 kiloDaltons.

After the enzymatic digestion step, the resulting hydrolysate isfiltered in order to remove undigested material which may be collectedand returned to another round of enzymatic digestion. The separationstep may be performed using a number of methods to separate outundigested material of a given size. In one embodiment, the hydrolysateis passed through a mesh attached to an agitator, e.g., a vibratorysieve. The size of the undigested material that is separated from thehydrolysate is determined by the size of the openings created by themesh or sieve. In representative embodiments, the size of the openingsin the mesh or sieve precludes objects of greater than 10, 20, 30, 40,50, 60 70, 80, 90, 100, 110, 120, 130, 140, 149, 150, 160, 170, 180,190, 200, 300, 400, 500, 600, 700, 800, 900 microns or more in diameter,such as objects greater than 0.1, 0.2, 0.3, 0.4, 0.5, 0.6, 0.7, 0.8,0.9, 1, 2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17, 18, 19,20, 30, 40, 50, 60, 70, 80, 90, 100, 110, 120, 130, 140, 150, 160, 170,180, 190, 200, 300, 400, 500 or 1000 millimeters in diameter or anyrange in between. In another embodiment, the hydrolysate may beseparated using known methods, such as centrifugation, filter press, orair classifier methods.

The hydrolysate in which undigested organic matter of a specified sizehas been separated may subsequently be subjected to a stabilizationstep. In one embodiment, the hydrolysate is stabilized with acid (e.g.,liquid acid sources including, for example, hydrochloric, sulfuric,phosphoric, acetic, stearic, propionic, tartaric, maleic, benzoic, orsuccinic acids) such that the hydrolysate has a pH of less than 7.0. Inanother embodiment, the acidic pH of the hydrolysate is 3.5. Low pHinhibits microbial and/or pathogenic activity during storage andtransport of the hydrolysate. An acid source is thoroughly blended inwith the hydrolysate for some amount of time (e.g., for at least 2hours, 4 hours, 8 hours, 12 hours, 16 hours, 24 hours, or longer) inorder to stabilize the pH.

The stabilized hydrolysate may be separated in order to removeundigested material. The separation step may be performed using a numberof methods to separate out undigested material of a given size. In oneembodiment, the hydrolysate is passed through a mesh attached to anagitator, e.g., a mechanical agitator. The size of the undigestedmaterial that is separated from the hydrolysate is determined by thesize of the openings created by the mesh. In representative embodiments,the size of the openings in the mesh or sieve precludes objects ofgreater than 10, 20, 30, 40, 50, 60 70, 80, 90, 100, 110, 120, 130, 140,149, 150, 160, 170, 180, 190, 200, 300, 400, 500, 600, 700, 800, 900microns or more in diameter, such as objects greater than 0.1, 0.2, 0.3,0.4, 0.5, 0.6, 0.7, 0.8, 0.9, 1, 2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 13,14, 15, 16, 17, 18, 19, 20, 30, 40, 50, 60, 70, 80, 90, 100, 110, 120,130, 140, 150, 160, 170, 180, 190, 200, 300, 400, 500 or 1000millimeters in diameter or any range in between. In one embodiment, thesize of the openings in the mesh precludes objects of greater than 149microns in diameter, as this ensures that the resulting hydrolysate willbe able to flow unimpeded through hydrolysate applicators, such as dripirrigation, spray rig, and fertigation equipment without generating. Inanother embodiment, the hydrolysate may be separated using knownmethods, such as centrifugation, filter press, or air classifiermethods.

The filtered hydrolysate may be marketed in suitable containers such asplastic or metal drums or it may be transported in bulk in tanks. Priorto transport, the filtered hydrolysate may be checked in a qualitycontrol step including, for example, analyses of pH and gas levels. Thefiltered hydrolysate may also be used in a variety of manners,including, for example, as nutraceuticals, organic fertilizers,pharmaceuticals, aquaculture feeds, animal feeds, and biostimulants. Inone embodiment, additives may be added to alter the qualities of thefiltered hydrolysate (e.g., addition of kelp, molasses, and humicacids). In other embodiments, the hydrolysate may be concentrated suchthat the hydrolysate has a dry solid residue cocnentration of at least5%, 10%, 15%, 20%, 25%, 30%, 35%, 40%, 45%, 50%, 55%, 60%, 65%, 70%,75%, 80%, 85%, 90%, 95%, 99%, or greater or any range in between. Forexample, the concentration may be performed in a system for continuousconcentration under vacuum, the degree of concentration being monitoredby a mass measuerer. Alternatively, the hydrolysate may be concentratedto dryness, for example, by spray-drying, thus producing a final productin powder form.

The separated hydrolysate resulting from the enzymatic digestion processdescribed herein, alone or further processed according to the optionalsteps described herein, allows for the recovery of nutrients fromdigested organic waste, e.g., fresh food waste, in a bioavailable form.Such processing conditions the nutrients for relatively rapid uptake bysoil microorganisms and plants, as contrasted with the more extendedperiod required for bio-degrading the cellular components of manures andorganic wastes incorporated into soils as fertilizers. Such processingalso conditions the nutrients for rapid metabolization when the filteredhydrolysate is used as an aquaculture or animal feed.

In one embodiment, the process described herein may be adapted andcoupled with a process for producing biofuels, such as biogas oralcohols. The concentrated nutrient availability in a bioavailable formrepresents an enhanced feedstock for biogas producing microorganisms.The hydrolysate may thus be used by one or more microorganisms toproduce fermentation products such as ethanol. Any microorganism capableof converting a carbon source (e.g., glucose) to a biofuel (e.g.,ethanol) may be used in the process according to the invention. Forexample, a suitable microorganism may be a mesophilic microorganism(i.e. one which grows optimally at a temperature in the range of 20-40°C.), e.g. a yeast also referred to as “baker's yeast”, Saccharomycescerevisiae.

It will be understood, that a useful ethanol-fermenting organism may beselected from a genetically modified organism of one of the above usefulorganisms having, relative to the organism from which it is derived, anincreased or improved useful chemical forming activity (e.g.,biofuel-fermenting activity).

An anaerobic or aerobic fermentation may employ one or more fermentingmicroorganisms capable of degrading or converting substances present inthe organic waste to form, e.g., combustible fuel, such as methane. Inone embodiment of the present invention, an initial treatment of thewaste is performed using methane-producing microorganisms (also known asmethanogens), which constitute a group of prokaryotes that are capableof forming methane from certain classes of organic substrates, methylsubstrates or acetate under anaerobic conditions. It will be appreciatedthat useful methanogenic bacteria may be selected from a geneticallymodified bacterium of known methanogenic bacteria, having, relative tothe organism from which it is derived, an increased or improved methaneproducing activity. Other useful microorganisms which could be used inan anaerobic fermentation of the waste include certain fermentativeanaerobic bacteria capable of converting, for example, glucose toproducts such as acetate, propionate, butyrate, hydrogen and CO₂, andso-called acetogenic bacteria, which convert organic substances such aspropionate, butyrate and ethanol to acetate, formate, hydrogen and CO₂.

The process according to the invention is in particular suitable forapplications coherent with large-scale waste management systems. Whenthe process is performed for downstream biogas production, excess heatfrom the biogas production plant may be utilized as process energy inthe incubation processes.

In a further aspect, the present invention provides the nutritionalelement obtained in the process (e.g. hydrolysate) according to theinvention for use as nutraceuticals, organic fertilizers,pharmaceuticals, aquaculture feeds, animal feeds, and biostimulants.

In yet another aspect, the present invention provides an enzyme mixturecomprising at least two enzymes, e.g., three, four, five, six, seven,eight, nine or ten enzymes, selected from the group consisting ofxylanase, asparaginase, cellulase, hemicellulase, glumayase,beta-glumayase (endo-1,3(4)-), urease, protease, lipase, amylase,phytase, phosphatase, aminopeptidase, amylase, carbohydrase,carboxypeptidase, catalase, chitinase, cutinase, cyclodextringlycosyltransferase, deoxyribonuclease, esterase, alpha-galactosidase,beta-galactosidase, glucoamylase, alpha-amylase, alpha-glucosidase,beta-glucosidase, haloperoxidase, invertase, laccase, mannosidase,oxidase, pectinolytic enzyme, peptidoglutaminase, peroxidase,polyphenoloxidase, proteolytic enzyme, protease, ribonuclease andtransglutaminase, or combinations thereof.

In a still further aspect, the invention relates to the use of theenzyme mixture according to the invention for releasing nutritionalelements from waste.

This invention is further illustrated by the following examples whichshould not be construed as limiting. The contents of all references,patents and published patent applications cited throughout thisapplication are incorporated herein by reference.

EXAMPLES Example 1

The following example describes an exemplary process for releasingnutritional elements in a bioavailable form from enzymatic digestion offresh organic waste. Fresh organic waste is obtained and handled so asto minimize biological degradation, which includes the steps of frequentwaste pickup(e.g., before 36 hours after discarding as elapsed),materials are kept refrigerated at all times, training personnel onsource separation and being able to identify decomposition and properuse of the specialized containers, and specialized waste containersspecifically designed for each waste stream. The fresh food waste isground to particles less than ½ inch in length. An enzyme cocktailcomprising 1 gram (i.e., the weight of 50 mL of enzyme given that thedensity of the enzymes solutions is similar to that of water) of eachenzyme (e.g., 1 g of Asparaginase (3,500 ASNU/g, Acrylaway® L,Novozymes, Inc.), 1 g of Beta-glucanase (endo-1,3(4)-) (100 FBG/g,Peelzym® or Viscozyme® L, Novozymes, Inc.), 1 g of Cellulase (700 EGU/g,Celluclast®, 1.5L, Lot #CCN03079, Novozymes, Inc.), 1 g of Protease (2.4AU-A/g, Alcalase 2.4 LFG®, Lot #PLN05317, Novozymes, Inc.), 1 g ofAlpha-amylase (400 KNU-B/g, Ban 480L®, Lot #ADN04234, Novozymes, Inc.),and 1 g of Lipase (100 KLU/g, Greasex 100L®, Lot #LAP40013, Novozymes,Inc.) is added per 8×10⁴ gram of organic waste to be enzymaticallydigested. The mixture is then added to a digestion tank an allowed toincubate for up to 2.5 hours, generally between 45 minutes and 1.5hours, and at a temperature of between 125° F. and 140° F. underconstant stirring and atmospheric pressure. The mixture is incubatedsuch that a resulting liquid hydrolysate is typically greater than 90%or 95% or more by weight relative to the weight of the initial organicwaste loaded. The hydrolysate is generally filtered from coarsematerials greater than 1/16^(th) in. in diameter by mechanical agitationand separation through a mesh. The coarse-filtered hydrolysate issubsequently pumped to intermediate storage tanks and mixed with acid inthe ratio of 20 liters acid to 1000 liters of hydrolysate for 4 hours orlonger until the pH is less than 7.0 (e.g., until the pH is 3.5). Afteracid stabilization, the liquid hydrolysate is fine-filtered bymechanical agitation and separation through a mesh comprising pores of100 US Sieve Mesh, which excludes particles larger than 149 microns.Excluded material resulting from either of the filtration steps may bere-digested, composted, or used as a substrate for anaerobic digestion.The fine-filtered hydrolysate is pumped into storage tanks until readyfor dispensation into smaller volumes for transport and sale.

Example 2

The following example demonstrates that nutritional elements arereleased in a bioavailable form upon execution of the processes asdescribed herein. Unground material, using only alcalaise enzymesproduces a 66% yield of hydrolysate. The same yield was achieved whenprocessed at 125° F., 13° F., 14° F., and 160° F. Each temperature rangewas checked at 30 minutes intervals to determine what percentage ofhydrolysate was being achieved. Each digest was allowed to run for 3½hours before the experiment was stopped. Each test produced a yield of66% +/−2%.

The same tests were run as above with unground material and usingalcalaise and nature pepsim from squalus amaythias. Yields from eachtest improved slightly to 71% +/−2%. Unground material was subsequentlyprocessed at the same temperature and time ranges as above using the 6enzymes (main enzymes) from Lew's selection as well as natural pepsimfrom squalus amaythias and resulted in a maximum yield of 78% at 145° F.for 2.5 hours. Finally, material ground to less than ⅜″ in diameter,when processed using the using the same enzyme set as the previous test,as well as the same time and temperature range, produced a yield of 95%.

INCORPORATION BY REFERENCE

All publications, patents, and patent applications mentioned herein arehereby incorporated by reference in their entirety as if each individualpublication, patent or patent application was specifically andindividually indicated to be incorporated by reference. In case ofconflict, the present application, including any definitions herein,will control.

Equivalents

Those skilled in the art will recognize, or be able to ascertain usingno more than routine experimentation, many equivalents to the specificembodiments of the invention described herein. Such equivalents areintended to be encompassed by the following claims.

1. A process for the release of nutritional elements from organic wastecomprising the steps of: (a) adding to said organic waste at least oneenzyme or at least one mixture of enzymes; (b) incubating the organicwaste of step (a) under appropriate conditions resulting in at leastpartial release of the nutritional elements as a liquid hydrolysate; and(c) separation of the undigested waste from the resulting liquidhydrolysate.
 2. The process of claim 1, wherein the organic waste isfresh food waste.
 3. The process of claim 1, wherein at least two ormore, such as three, four, five, six, seven, eight, nine, or ten enzymesare added to the organic waste in step (a).
 4. The process of claim 3,wherein the two or more enzymes are added together or sequentially tothe organic waste in step (a).
 5. The process of claim 4, wherein thetwo or more enzymes are selected from the group consisting of xylanase,asparaginase, cellulase, hemicellulase, glumayase, beta-glumayase(endo-1,3(4)-), urease, protease, lipase, amylase, phytase, phosphatase,aminopeptidase, amylase, carbohydrase, carboxypeptidase, catalase,chitinase, cutinase, cyclodextrin glycosyltransferase,deoxyribonuclease, esterase, alpha-galactosidase, beta-galactosidase,glucoamylase, alpha-amylase, alpha-glucosidase, beta-glucosidase,haloperoxidase, invertase, laccase, mannosidase, oxidase, glucoseoxidase, pectinolytic enzyme, pectinesterase, peptidoglutaminase,peroxidase, polyphenoloxidase, proteolytic enzyme, protease,ribonuclease and transglutaminase.
 6. The process of claim 1, whereinthe enzymes are selected from the group consisting of enzymesoriginating from microbial fermentation, enzymes derived from amicroorganism, and enzymes derived from plants.
 7. The process accordingto claim 1, wherein the incubating organic waste of step (b) is under aconstant movement.
 8. The process according to claim 1, wherein thetemperature of the incubating organic waste of step (b) is between 70°F. and 162° F.
 9. The process according to claim 8, wherein thetemperature of the incubating organic waste of step (b) is between 125°F. and 140° F.
 10. The process according to claim 1, wherein theincubating organic waste of step (b) is incubated for between 0 hoursand 2.5 hours.
 11. The process according to claim 10, wherein theincubating organic waste of step (b) is incubated for between 45 minutesand 1.5 hours.
 12. The process according to claim 1, wherein theincubating organic waste of step (b) outputs a liquid hydrolysate thatis greater than 70 percent by weight relative to the weight of the inputincubating organic waste.
 13. The process according to claim 13, whereinthe incubating organic waste of step (b) outputs a liquid hydrolysatethat is greater than 90 percent by weight relative to the weight of theinput incubating organic waste.
 14. The process according to claim 1,wherein the separation step of step (c) excludes undigested material ofgreater than 1 millimeter in diameter from the liquid hydrolysate. 15.The process according to claim 14, wherein the separation step of step(c) excludes undigested material of greater than 0.5 millimeter indiameter from the liquid hydrolysate.
 16. A process for the release ofnutritional elements from organic waste comprising the steps of: (a)adding to said organic waste at least one enzyme or at least one mixtureof enzymes; (b) incubating the organic waste of step (a) underappropriate conditions resulting in at least partial release of thenutritional elements as a liquid hydrolysate; (c) separation of theundigested waste from the resulting liquid hydrolysate; and (d)stabilization of the liquid hydrolysate resulting from step (c).
 17. Theprocess of claim 16, wherein the organic waste is fresh food waste. 18.The process of claim 16, wherein at least two or more, such as three,four, five, six, seven, eight, nine, or ten enzymes are added to theorganic waste in step (a).
 19. The process of claim 18, wherein the twoor more enzymes are added together or sequentially to the organic wastein step (a).
 20. The process of claim 19, wherein the two or moreenzymes are selected from the group consisting of xylanase,asparaginase, cellulase, hemicellulase, glumayase, beta-glumayase(endo-1,3(4)-), urease, protease, lipase, amylase, phytase, phosphatase,aminopeptidase, amylase, carbohydrase, carboxypeptidase, catalase,chitinase, cutinase, cyclodextrin glycosyltransferase,deoxyribonuclease, esterase, alpha-galactosidase, beta-galactosidase,glucoamylase, alpha-amylase, alpha-glucosidase, beta-glucosidase,haloperoxidase, invertase, laccase, mannosidase, oxidase, glucoseoxidase, pectinolytic enzyme, pectinesterase, peptidoglutaminase,peroxidase, polyphenoloxidase, proteolytic enzyme, protease,ribonuclease and transglutaminase.
 21. The process of claim 16, whereinthe enzymes are selected from the group consisting of enzymesoriginating from microbial fermentation, enzymes derived from amicroorganism, and enzymes derived from plants.
 22. The processaccording to claim 16, wherein the incubating organic waste of step (b)is under a constant movement.
 23. The process according to claim 16,wherein the temperature of the incubating organic waste of step (b) is70° F. and 162° F.
 24. The process according to claim 23, wherein thetemperature of the incubating organic waste of step (b) is 125° F. and140° F.
 25. The process according to claim 16, wherein the incubatingorganic waste of step (b) is incubated for 0 and 2.5 hours.
 26. Theprocess according to claim 25, wherein the incubating organic waste ofstep (b) is incubated for 45 minutes and 1.5 hours.
 27. The processaccording to claim 16, wherein the incubating organic waste of step (b)outputs a liquid hydrolysate that is greater than 70 percent by weightrelative to the weight of the input incubating organic waste.
 28. Theprocess according to claim 27, wherein the incubating organic waste ofstep (b) outputs a liquid hydrolysate that is greater than 90 percent byweight relative to the weight of the input incubating organic waste. 29.The process according to claim 16, wherein the separation step of step(c) excludes undigested material of greater than 1 millimeter indiameter from the liquid hydrolysate.
 30. The process according to claim29, wherein the separation step of step (c) excludes undigested materialof greater than 0.5 millimeter in diameter from the liquid hydrolysate.31. The process according to claim 16, wherein the stabilization step ofstep (d) comprises addition and mixing of the liquid hydrolysate with anacid source.
 32. The process according to claim 31, wherein the acidsource is selected from the group consisting of hydrochloric, sulfuric,phosphoric, acetic, stearic, propionic, tartaric, maleic, benzoic, orsuccinic acids.
 33. The process according to claim 31, wherein the pH ofthe liquid hydrolysate is less than 7.0.
 34. The process according toclaim 33, wherein the pH of the liquid hydrolysate is 3.5.
 35. A processfor the release of nutritional elements from organic waste comprisingthe steps of: (a) adding to said organic waste at least one enzyme or atleast one mixture of enzymes; (b) incubating the organic waste of step(a) under appropriate conditions resulting in at least partial releaseof the nutritional elements as a liquid hydrolysate; (c) coarseseparation of the undigested waste from the resulting liquidhydrolysate; (d) stabilization of the liquid hydrolysate resulting fromstep (c); and (e) fine separation of the undigested waste from theresulting liquid hydrolysate.
 36. The process of claim 35, wherein theorganic waste is fresh food waste.
 37. The process of claim 35, whereinat least two or more, such as three, four, five, six, seven, eight,nine, or ten enzymes are added to the organic waste in step (a).
 38. Theprocess of claim 37, wherein the two or more enzymes are added togetheror sequentially to the organic waste in step (a).
 39. The process ofclaim 38, wherein the two or more enzymes are selected from the groupconsisting of xylanase, asparaginase, cellulase, hemicellulase,glumayase, beta-glumayase (endo-1,3(4)-), urease, protease, lipase,amylase, phytase, phosphatase, aminopeptidase, amylase, carbohydrase,carboxypeptidase, catalase, chitinase, cutinase, cyclodextringlycosyltransferase, deoxyribonuclease, esterase, alpha-galactosidase,beta-galactosidase, glucoamylase, alpha-amylase, alpha-glucosidase,beta-glucosidase, haloperoxidase, invertase, laccase, mannosidase,oxidase, glucose oxidase, pectinolytic enzyme, pectinesterase,peptidoglutaminase, peroxidase, polyphenoloxidase, proteolytic enzyme,protease, ribonuclease and transglutaminase.
 40. The process of claim35, wherein the enzymes are selected from the group consisting ofenzymes originating from microbial fermentation, enzymes derived from amicroorganism, and enzymes derived from plants.
 41. The processaccording to claim 35, wherein the incubating organic waste of step (b)is under a constant movement.
 42. The process according to claim 35,wherein the temperature of the incubating organic waste of step (b) is70° F. and 162° F.
 43. The process according to claim 42, wherein thetemperature of the incubating organic waste of step (b) is 125° F. and140° F.
 44. The process according to claim 35, wherein the incubatingorganic waste of step (b) is incubated for between 0 hours and 2.5hours.
 45. The process according to claim 44, wherein the incubatingorganic waste of step (b) is incubated for between 45 minutes and 1.5hours.
 46. The process according to claim 35, wherein the incubatingorganic waste of step (b) outputs a liquid hydrolysate that is greaterthan 70 percent by weight relative to the weight of the input incubatingorganic waste.
 47. The process according to claim 46, wherein theincubating organic waste of step (b) outputs a liquid hydrolysate thatis greater than 90 percent by weight relative to the weight of the inputincubating organic waste.
 48. The process according to claim 35, whereinthe separation step of step (c) excludes undigested material of greaterthan 1 millimeter in diameter from the liquid hydrolysate.
 49. Theprocess according to claim 48, wherein the separation step of step (c)excludes undigested material of greater than 0.5 millimeter in diameterfrom the liquid hydrolysate.
 50. The process according to claim 35,wherein the stabilization step of step (d) comprises addition and mixingof the liquid hydrolysate with an acid source.
 51. The process accordingto claim 50, wherein the acid source is selected from the groupconsisting of hydrochloric, sulfuric, phosphoric, acetic, stearic,propionic, tartaric, maleic, benzoic, or succinic acids.
 52. The processaccording to claim 50, wherein the pH of the liquid hydrolysate is lessthan 7.0.
 53. The process according to claim 52, wherein the pH of theliquid hydrolysate is 3.5.
 54. The process according to claim 35,wherein the separation step of step (e) excludes undigested material ofgreater than 300 microns in diameter from the liquid hydrolysate. 55.The process according to claim 54, wherein the separation step of step(e) excludes undigested material of greater than 149 microns in diameterfrom the liquid hydrolysate.
 56. The process according to claims 1, 16,or 35, wherein the organic waste of step (a) is first ground intoparticles less than ⅜ inch in diameter.
 57. The process according toclaims 1, 16, or 35, wherein the liquid hydrolysate is used as anutraceutical, organic fertilizer, pharmaceutical, aquaculture feed,animal feed, or biostimulant.